ii PRODUCTION AND CHARACTERIZATION OF BIO OIL FROM ...
Transcript of ii PRODUCTION AND CHARACTERIZATION OF BIO OIL FROM ...
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PRODUCTION AND CHARACTERIZATION OF BIO OIL FROM WOOD SAWDUST VIA FAST PYROLYSIS
SANDRA DIANA BINTI MD ZIN
Thesis submitted in fulfillment of the requirements
for the award of the degree of
Bachelor of Chemical Engineering in Gas Technology
Faculty of Chemical & Natural Resources Engineering
UNIVERSITY MALAYSIA PAHANG
DECEMBER 2010
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ABSTRACT
In this study, the production and characterization of bio oil from wood sawdust via fast pyrolysis was investigated. In fast pyrolysis of wood sawdust, the yields of the products were studied to elucidate the effect of the process parameters such as pyrolysis temperatures, nitrogen (N2) gas flow rate and pyrolysis holding time. This research was carried out in a design electric furnace reactor and heated externally. The yields product from this experiment were collected and analyzed. The experiments were conducted at a temperature range of 450-550 ⁰C. The holding time was varied in the range 1-5 minutes, and the nitrogen (N2) gas flow rate was varied in the range of 1-3 liter/min. The general characteristic of the product was investigated by the determination of the functional groups present in the bio oil using Fourier Transform Spectroscopy (FTIR). The best conditions to produce bio oil from various parameters that give the highest product yield were at temperature 500 ⁰C, 1 minute of holding time and 3 liter/min of nitrogen (N2) gas flow rate. The maximum yield of bio oil produced from these conditions was 44.6%. From the analysis, it was shown that the pyrolysis oils contain complex compounds mostly functional groups of phenol, alcohols, ketones, aldehydes and carboxylic acids aromatic and also carbonyl structures.
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ABSTRAK
Dalam kajian ini, penghasilan dan ciri-ciri yang minyak bio dari serbuk kayu melalui pirolisis pantas diselidiki. Dalam pirolisis pantas dari serbuk gergaji kayu, hasil dari produk tersebut dikaji untuk menjelaskan pengaruh parameter proses seperti suhu pirolisis, (N2) laju alir gas nitrogen dan masa pegangan. Kajian ini telah dijalankan menggunakan reaktor tiub yang direka dan dipanaskan menggunakan elektrik dari luar. Produk hasil dari percubaan ini dikumpul dan dianalisa. Percubaan dilakukan pada suhu di antara 450-550 ⁰ C. Masa pegangan divariasikan dalam julat 1-5 minit, dan laju alir gas nirogen (N2) yang berbeza-beza di antara 1-3 liter/minit. Ciri-ciri umum produk ini digunakan untuk menentukan kumpulan berfungsi yang hadir dalam minyak bio dengan menggunakan Fourier Transformasi Spektroskopi (FTIR). Keadaan terbaik untuk menghasilkan minyak bio dari berbagai parameter yang memberikan hasil produk yang tertinggi ialah pada pada suhu 500 ⁰ C, 1 minit masa pegangan dan 3 liter/minit laju aliran gas nitrogen (N2). Keputusan maksimum minyak bio yang dihasilkan dari keadaan ini adalah sebanyak 44.6%. Dari analisis, di dapati bahawa minyak pirolisis mengandungi sebatian kompleks yang sebahagian besarnya terdiri dari kumpulan berfungsi fenol, alkohol, keton, aldehid dan asid karboksilik aromatik dan juga struktur karbonil.
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TABLE OF CONTENTS
CHAPTER TITLE PAGE
TITLE PAGE ii
DECLARATION iii
DEDICATION iv
AKNOWLEDGEMENT v
ABSTRACT vi
ABSTRAK vii
TABLE OF CONTENTS viii
LIST OF TABLES xi
LIST OF FIGURES xii
LIST OF ABBREVIATIONS xiii
1 INTRODUCTION
1.1 Background of Study 1
1.2 Problem Statement 3
1.3 Objective of Study 4
1.4 Scope of Research 5
2 LITERATURE REVIEW
2.1 Biomass 6
2.2Biofuel and Impact to Environment 8
2.3 Wood Sources 9
2.3.1 Wood Sawdust 9
2.3.2 Wood Sawdust Properties 10
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2.4 Technology Description 11
2.5 Thermal Conversion Process 11
2.5.1 Combustion 13
2.5.2 Gasification 13
2.5.3 Pyrolysis 13
2.6 Pyrolysis Process Types 14
2.6.1 Slow Pyrolysis 14
2.6.2 Fast Pyrolysis 17
2.7 Pyrolysis Product 20
2.7.1 Bio oil 20
2.7.2 Char 23
2.7.3 Gas 24
2.8 Characterization of Bio oil 24
2.9 Pyrolysis Product Application 26
2.9.1 Uses of Bio oil 26
2.9.2 Uses of Char 28
2.9.3 Uses of Gas 28
3 METHODOLOGY
3.1 Introduction 29
3.2 Material and Apparatus 31
3.2.1 Raw Material 31
3.2.2 Pyrolysis Apparatus 32
3.3 Experimental Procedures 34
3.3.1 Sample Preparation 34
3.3.2 Bio Oil Production 34
3.3.3 Analysis of Product 34
4 RESULTS AND DISCUSSION
4.1 Yield of Product 35
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4.1.1 The Effect of Temperature 35
4.1.2 The Effect of Holding Time 38
4.2.3 The Effects of N2 Flow Rate 41
4.2 Characterization of Bio Oil 44
4.2.1 FTIR 44
5 CONCLUSION AND RECOMMENDATION
5.1 Conclusion 48
5.2 Recommendation 49
REFERENCES 50
APPENDIX
Appendix A1 59
Appendix A2 60
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LIST OF TABLES
TABLE NO. TITLE PAGE
2.1 Percent yields of products (approx.) from various 15
biomasses at different temperatures
2.2 Variation of product with temperature for cottonseed cake 16
2.3 Product yield varying with temperature and particle size 16
2.4 Typical product yields (dry wood basis) obtained 17 by different modes of pyrolysis of wood 2.5 Percent yield (approx.) with variable particle 19 size and temperature 2.6 Effect of biomass species on bio-oil production 20
2.7 Relative content of main compounds in organic 26 composition of bio-oil produced from P. indicus 3.1 Proximate and ultimate analyses of sawdust and coal 32
4.1 Operating condition and result (temperature) 36 4.2 Operating condition and result (holding time) 39 4.3 Operating condition and result (N2 flow rate) 41
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LIST OF FIGURES
FIGURE NO. TITLE PAGE
2.1 Products from thermal bio mass conversion 12
3.1 Flow chart of methodology 30
3.2 Wood Sawdust 31
3.3 Schematic diagram of the pyrolysis apparatus 33
4.1 Effect of Temperature on product yields 36 4.2 Effect of holding time on product yields 39 4.3 Effect of N2 flow rate on product yields 42 4.4 FTIR Spectra of Bio-oil at Different Temperature 45 4.5 FTIR Spectra of Bio-oil at Different Holding time 46
4.6 FTIR Spectra of Bio-oil at Different Nitrogen Flow Rate 47
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LIST OF ABBREVIATIONS
BCO bio-crude oil C2H4 ethylene C2H6 ethane C5H8O4 xylem C6H10O3.OCH3 hemicelluloses C6H10O5 cellulose CH4 methane CO carbon monoxide CO2 carbon dioxide cP centipoise FTIR fourier transform infra ied GC gas chromatography H2 hydrogen H2O water HCl hydrochloric acid IGCC integrated gasification combined cycle IR infra red LPM litre per minute mPa.s milipascal-second MW megawatt N2 nitrogen N2O nitrous oxide NMR nuclear magnetic resonance NOx nitrogen oxide NREL National Renewable Energy Laboratory O2 oxygen
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PAHs polycyclic aromatic hydrocarbon PID proportional–integral–derivative SO2 sulphur dioxide SOx sulphur oxide UMP University Malaysia Pahang UV ultraviolet
CHAPTER 1
INTRODUCTION
1.1 Background Of Study
Energy comes in a variety of renewable forms; wood, biomass, wind,
sunlight. It also comes in the nonrenewable form of fossil fuels- oil and coal and their use is
a major source of pollution of land, sea and above all the air we breathe. Two centuries of
unprecedented industrialization, driven mainly by fossil fuels, have changed the face of this
planet. The present civilization cannot survive without motor cars and electricity. The
increasing rate at which the changes in human lives are occurring has important
consequences for the environment and carrying capacity of earth. The industrial revolution
has brought greatly increased wealth to one quarter of the population and severe
inequalities. Pollution and accelerating energy consumption has already affected
equilibrium of earth land masses, oceans and atmosphere. Particularly, important is the loss
of biodiversity. Fortunately, the last 25 years has seen growing awareness of some of these
consequences.
Renewable energy is of increasing consequence in satisfying environmental
concerns over fossil fuel usage. It also considered as a very vital contributors to the energy
supply in global as they contribute to energy supply security, reducing dependency on fossil
fuel resources, and also provides an opportunities for mitigating greenhouse gases. This
energy can be generated from natural resources such as sunlight, wind, rain, and geothermal
heat, which are renewable. Basically this energy is used to generate electricity or produce
heat in much application, especially in industrial area.
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Modern agriculture is an extremely energy intensive process. However high
agricultural productivities and subsequently the growth of green revolution has been made
possible only by large amount of energy inputs (Leach, 1976). With recent price rise and
scarcity of these fuels there has been a trend towards use of alternative energy sources like
solar, wind, geothermal etc (Rajvanshi, 1978). However these energy resources have not
been able to provide an economically viable solution for agricultural applications (Dutta,
1981).
Since the energy crisis in 1970s, the energy utilization from biomass resources
(called biomass energy) has received much attention. The energy obtained from agricultural
wastes or agricultural residues is a form of renewable energy and, in principle, utilizing this
energy does not add carbon dioxide (CO2), which is a greenhouse gas, to the atmospheric
environmental pollution and health risk than fossil fuel combustion (McKendry, 2002).
As we can see, nowadays, biomasses becomes the world’s primary renewable and
source of energy replacing fossil fuels such as oil, natural gas and coal which had been our
foremost energy demand for a long time ago. This highest potential biomass is considered
the renewable energy source that contributed to the energy desires of modern society for
both the developed and developing economies global. Biomass is a major source of energy
for mankind and is presently estimated to contribute of the order of 10%-14% of the world's
power supply. Its typically possesses higher hydrogen content and a larger volatile
component and produces a more reactive char after devolatilization or pyrolysis. It contains
lower ash and sulfur contents (Guo, 2004).
Biomass may vary in its physical and chemical properties due to its diverse origin
and species. However, biomass is structurally composed of cellulose, hemicellulose, lignin,
extractives and inorganics. From the chemistry point of view, biomass is composed of
series of long chain hydrocarbons with functional groups such as hydroxyls and carboxyls
(Sukiran, 2008)
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The main advantages of using this biofuel are its renewability, as it gives a better
quality exhaust gas emission, its biodegradability and, it does not contribute to a net rise in
the level of CO2 in the atmosphere, and consequently to the green house effect (Sensoz et
al., 2006)
Additionally, biomass, when grown and converted in a closed-loop feedstock
production scheme, generates no net CO2 emissions, thereby claiming a neutral position in
the build-up of atmospheric greenhouse gases. Also, biomasses offer the only source of
renewable liquid, gaseous and solid fuels. The fuels and residues that come from the
biomass can be converted to energy through several processes which are thermal, biological
and physical processes (Guo, 2004).
1.2 Problem Statement
In this century, it is believed that the crude oil and petroleum products will become
very scarce and costly. Day to day, fuel economy of engine is getting improved and will
continue to improve. However, enormous increases in number of vehicles have started
dictating the demand for fuel. Gasoline and diesel will become scarce and most costly in
the near future. With increased use and the depletion of fossil fuels, alternative fuel
technology will become more common in the coming decades (Behera, 2010).
The scientific consensus on global warming is clear. If atmospheric concentrations
of greenhouse gases continue to rise in this century the way they did during the twentieth
century, global ecosystems will be disrupted in ways that will alter the environmental
conditions in which human civilizations have developed and thrived (Morris et al., 2001).
Also, concerning the depletion of fossil fuels worldwide and the increasing environmental
pollution, numerous endeavors have been attempted to find other renewable and
environmental friendly energy sources and to advance the technologies (Guo, 2004).
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Malaysia is blessed with natural resources, particularly crude oil and natural gas,
which are the main sources of energy. However, these are depleting energy resources and
increasing demand has made it necessary for the Government to embark on alternative
energy sources. Rising crude oil prices have led to higher government expenditures on
subsidies to keep retail fuel prices at relatively low levels (Economic Report 2006/2007,
2007).
The rapid climate change and the need to manage diminishing fossil fuel reserves
are the latest biggest challenges facing by our planet. In order to secure the future for
ourselves and generations to follow, we must take a drastic act now in order to reduce
energy consumption and substantially cut greenhouse gases problem, such as the emission
and high CO2 content in the atmosphere. This environmental strain caused by fossil fuel
make an effort from many industries to find an alternative fuel that focused on sources of
raw material based on renewable resources.
Towards this direction, the oil obtained by using a method of pyrolysis of renewable
biomass was seen as an attractive substitute for the limited supply fossil fuels and possibly
to be use an alternative sources. Wood sawdust is one of the biomass wastes that come
from agriculture activities which composed of fine particles of wood and it can be used for
renewable energy or fuel feedstock production. This kind of material is a byproduct from
cutting woods from the furniture factory as an example. There are several uses come from
this material such as mulch, an option to clay cat litter, for manufacture of particle board or
as a fuel. So, the explorations of the uses of wood sawdust as a main raw material in
producing bio-oil were investigated.
1.3 Objectives of Study
In the course of completing this project, there are few objectives to be fulfilled as follows:
1. To produce bio oil from wood sawdust via fast pyrolysis.
2. To investigate the effect of various pyrolysis parameters on product yields.
3. To analyze the characteristics of bio oil from wood sawdust.
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1.4 Scope of Study
The main idea behind this project would be:
• The production of bio oil from biomass. The formulation of bio-oil is obtaining
from a biological waste such wood sawdust via fast pyrolysis.
• Parameters that have been evaluated in this study were temperature (450-550 °C),
nitrogen (N2) / sweeping gas flow rate (1-3 litre/min) and holding time (1-5 minute)
to find the best operating.
• Characterizations of bio-oil produced from wood sawdust were then analyzed using
Fourier Transform Infra Red (FTIR).
CHAPTER 2
LITERATURE REVIEW
2.1 Biomass
Concerning the depletion of fossil fuels worldwide and the increasing
environmental pollution, numerous actions have been attempted to find other renewable
and environmental friendly energy sources and to advance the technologies. As to the
power generation, biomass fuels technology becomes one of the most promising
technologies in the last two decades.
Biomass, the name given to the plant matter which is created by photosynthesis,
includes firewood plantations, forestry residues, animal waste, agricultural residues, etc.
The supply of energy from biomass plays an increasing role in the debate on renewable
energies. The relative large amount of biomass has already used for energy generation that
reflects mainly the use of wood and traditional fuels in the developing countries.
Nevertheless, the use of biomass in industrialized countries is also significative (Zanzi,
2001 and Gercel, 2002).
The biomass resource also can be considered as organic matter, in which the energy
of sunlight is stored in chemical bonds. When the bonds between adjacent carbon,
hydrogen (H2) and oxygen (O2) molecules are broken by digestion, combustion, or
decomposition, these substances release their stored, chemical energy. Biomass has always
been a major source of energy for mankind and is presently estimated to contribute of the
order 10– 14% of the world’s energy supply (Guo, 2004).
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Biomass is derived from the reaction between carbon CO2 in the air, water (H2O)
and sunlight, via photosynthesis, to produce carbohydrates that form the building blocks
from biomass. Typically photosynthesis converts less than 1% of the available sunlight to
stored, chemical energy. The solar energy driving photosynthesis is stored in the chemical
bonds of the structural components of biomass. If biomass is processed efficiently, either
chemically or biologically, by extracting the energy stored in the chemical bonds and the
subsequent ‘energy’ product combined with O2, the carbon is oxidized to produce CO2 and
H2O. The process is cyclical, as the CO2 is then available to produce new biomass
(McKendry, 2002).
The energetic and industrial usage of biomass is becoming more and more
technologically and economically attractive. The use of biomass offers the advantages of
benefits, such as biomass is available in every country in various forms. Thus, assures a
secure supply of raw material to the energy system. Maintaining biomass as a significant
contributor to the national energy supply is for many countries, the best way of ensuring
greater autonomy and cheap energy for the industry. From environmental benefits, the
consumption of biomass for energy is an option for decreasing current environment
problems such an increase of CO2 in the atmosphere caused by the use of fossil fuels.
Furthermore, biofuels from biomass contain minimal sulphur, thus avoiding sulphur
dioxide (SO2) emissions. To be successful, alternative fuels is needed to give low emission
and rival gasoline and diesel in terms of cost, supply, and distribution, delivery to vehicles,
on-board storage and power density (Zanzi, 2001).
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2.2 Biofuel and Impact to Environment
At this time, biofuels are the most important type of renewable energy in road
transportation, but the argument over their environmental impact is continuing. Some argue
that when farming or in the process of growing plants, including deforestation and soil
acidification, is taken into account, biofuels consume more energy than they produce.
Biofuels, resulting from programs launched in the late 1970s to reduce oil
dependence, have been in industrial development for more than twenty years. Today, there
is strong renewed interest in biofuels: in the transport sector, they could lead to a reduction
in oil consumption and greenhouse gas emissions (Prieur et al., 2006)
Atmospheric gases such as CO2, nitrous oxide (N2O) and methane (CH4) can
regulate temperature of the earth. These greenhouse gases particularly CO2 allow energy
from the sun to penetrate to the earth, but trap the heat radiated from the earth’s surface.
Researchers, scientists and others are concerned about those gases being emitted to
atmosphere by human activities which will increase the global warming at a rate
extraordinary in human history. The CO2 emission from the usage of fossil fuels that
provide about 85% of the total world demand for primary energy, cause an increase of the
CO2 concentration in the atmosphere (Zanzi, 2001 and Gerkova et al., 1992). Another
acidic gaseous pollutant is hydrochloric acid (HCl) gas, produced from chlorine and mainly
associated with combustion of municipal wastes. HCl also plays an important role for
dioxin formation during combustion.
The use of biomass fuels in a closed carbon cycle as a substitute for fossil fuels, is
one of the most promising ways for tentative the increase of the CO2 concentration.
Biomass fuels make no net contribution to atmospheric CO2 if used sustainable to allow
regrowth (Onay et al., 2001). Biomass plays a significant role in reducing CO2 by acting
both as a reservoir of carbon, absorbing CO2 from the atmosphere during growth and as
direct substitute for fossil fuels. Furthermore, reforestations and introduction of alternative
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crops are needed to stop and revert phenomena like erosion and desertification (Zanzi, 2001
and Gercel 2002).
Special attention is being paid to the N2O emission from combustion of nitrogen-
containing fuels such as biomass, coal, peat or municipal waste. The N2O emission from
combustion of a nitrogen-containing fuel comes from two sources, thermal N2O and fuel
N2O. The formed from the nitrogen in the combustion air and its formation is more or less
dependent on the temperature and pressure in the combustor. The latter comes from the
oxidation of N2 in the fuel and is not particularly temperature sensitive. All the oxides of N2
also enhance the greenhouse effect (Zanzi, 2001).
2.3 Wood Sources
Wood is a ready source of fuel ever known to man. Its uses in both industry and
domestic purposes cannot be over emphasized. In most developing countries wood and
charcoal are the predominant fuels for preparation of food as well as serving as fuel for
small and medium scale industries (Zerbe, 2004 and Bhattacharya et al., 1999). Wood is
said to be the major renewable source of energy at present and the fourth largest source of
energy, for example rated after petroleum, coal and natural gas in that order, all of which
are non-renewable energy sources. In recent years, however, the high cost of oil and gas has
again induced people to burn more wood.
2.3.1 Wood Sawdust
Sawdust is the powdery wood waste produced by cutting wood with a saw. The size
of the sawdust particles depends on the kind of wood from which the sawdust is obtained
and also on the size of the teeth of the saw (Afuwape, 1983). In wood industries such as the
furniture industry or paper industry, a great amount of wood flakes and wood flours in the
form of sawdust are always found as wastes. These unused materials are usually applied as
a fuel source or for the manufacture of plywood.
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Malaysia contributes more than 50% of the world palm oil production. Palm tree
based plywood’s are increasingly used due to its environmental friendliness. Nearly
100,000 hectares of replanting is carried out every year. Several saw mills ranging from
small scale to large scale engaged in plywood production resulting generation of large
amount of saw dust. The saw dust generated during plywood processing finds extensive
applications in compressed powder boards, fuel pellets, mosquito coils, incense sticks,
activated carbon etc. Furthermore, large scale sawmills can utilize the sawdust for
cogeneration facility utilizing Integrated Gasification Combined Cycle (IGCC) technology
(Kannan, 2008).
2.3.2 Wood Sawdust Properties
The chemical composition of wood is an important parameter in determining the
energy value of wood materials. Wood is a composite of three basic polymers, namely
cellulose (C6H10O5 ), lignin (C6H10O3 ) (OCH3 ) and hemicelluloses such as xylem (C5H8O4
) (Tillman, 1978). Hard woods are deciduous trees or wide leafed trees, while soft woods
are coniferous trees which are cone-bearing evergreens. Hard wood generally contains
more energy than softwood on a dry weight basis due to higher lignin content plus the
presence of more resins in the extraction (Brown et al., 1952).
Specific heat capacity is the amount of heat energy required to raise the temperature
of a unit mass of a substance by one degree centigrade. Specific heat capacity differs from
one species of wood to another. Thermal conductivity is the measure of the rate at which
heat is conducted through the material; conductivity increases with the wood density. Wood
thermal conductivity is found to increase with higher moisture content (Panskin et al.,
1962).
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2.4 Technology Description
Biomass can be converted to biofuels which is a liquid and gaseous fuel such as
ethanol, methanol, gasoline, diesel fuel and methane.
Biomass fuels and residues can be converted to energy via thermal, biological and
physical processes. Each process area is described with the greatest highlighting on the
technologies that are attracting the most interest in the research and demonstration arenas.
In the thermochemical conversion technologies, biomass gasification has fascinated the
highest interest as it offers higher efficiencies compared to combustion and fast pyrolysis,
but it is still at a relatively early stage of development.
The energy potential from the biomass can be recovered either by direct use in
combustion systems or by improvement into a more valuable and utilizable fuel or gas or
higher-value products for the different industries. But the combustion of biomasses is not such
economical option. So the improvement by pyrolysis, liquefaction, or gasification becomes
more eye-catching and interesting. Biomass pyrolysis has been practiced for centuries in
the manufacture of charcoal, but only in the last time the physical and chemical processes
during pyrolysis were investigated (Gheorghe et al., 2009).
2.5 Thermal Conversion Processes
Thermochemical process is thought to have a great promise as a means for
efficiency and economically converting biomass into advanced value fuels. Biomass fuels
and residues can be converted to energy via thermal, biological and physical processes.
There are three main thermal processes available for converting biomass to a more useful
energy form which is combustion, gasification and pyrolysis. This thermochemical
conversion of biomass (pyrolysis, gasification, combustion) is one of the most promising
non-nuclear forms of future energy. It is renewable form with many ecological advantages
(Koufopanos et al., 1989). Each process gives their different range of products.
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In thermal conversion, combustion is already widely practiced. Gasification attracts
a high level of interest as it offers higher efficiencies compared to combustion. While fast
pyrolysis is interesting as a liquid is produced that offers advantages in storage and
transport and versatility in applications. The products and applications of these thermal
conversion processes are summarized in Figure 2.1.
Figure 2.1: Products from thermal bio mass conversion (Bridgwater, 2004)
The biodegradable fractions in wastes such as paper, wood, and food residue are
important sources of biomass for renewable-energy production through thermal or
biological conversion. While direct combustion is the dominant method applied to mixed
wastes, specific streams of industrial wastes with high energy content could be converted
into fuel feedstock using advanced techniques, such as pyrolysis and gasification. One
example of such materials is waste furniture, of which over 2.4 million tons were generated
in Korea in the past 3 years (Yoo, 2008).
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Although the wood in waste furniture could have been treated with paint, surface
coating, or pesticides, unlike fresh wood or forestry residues, it usually contains less
moisture and is available for pyrolysis and gasification after size reduction.
2.5.1 Combustion
Combustion of biomass and related materials is widely trained commercially and
economically justified to provide heat and power. The productions only satisfy the heat
market directly or power production via a Rankine cycle or similar (Bridgwater, 2004).
Efficiencies are low at small capacities and fouling and emissions are problematic in many
applications. The technology is commercially available and presents minimum risk to
investors. The product is heat, which must be used immediately for heat and/or power
generation as storage is not a viable option. Combustion of biomass processes heat the
biomass in the presence of unlimited O2. The products of the reaction are basically
additional heat, ash, and smoke.
2.5.2 Gasification
Gasification offers higher efficiencies at all scales of operation, and while on the
verge of being fully commercial still requires demonstration at commercially attractive
scales of operation (Bridgwater, 2004). Gasification heats the biomass to higher
temperatures (about 600-700 ⁰C) in an environment of limited O2. The biomass begins to
char and gives off a gaseous product that is a mixture of carbon monoxide (CO), H2, and
CH4.
2.5.3 Pyrolysis
Pyrolysis is thermal decomposition occurring in the absence of O2. It is always also
the first step in combustion and gasification processes where it is followed by total or
partial oxidation of the primary products. Lower process temperature and longer vapor
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residence times favor the production of charcoal. High temperature and longer residence
time increase the bio mass conversion to gas and moderate temperature and short vapor
residence time are optimum for producing liquids.
Pyrolysis lies at the heart of all thermochemical fuel conversion processes. It is eye-
catching because solid biomass and wastes, which are difficult and costly to manage, can be
readily converted to liquid products. Pyrolysis heats the biomass to temperatures (around
300-500 ⁰C) in the nonexistence of air. The biomass “melts” and vaporizes, producing
petroleum-like oil called “bio-oil.” This bio-oil can be transformed to gasoline or other
chemicals or materials.
These liquids have advantages in transport, storage, combustion, retrofitting and
flexibility in production and marketing. Pyrolysis also gives gas and solid (char) products,
the relative proportions of which depend very much on the pyrolysis method and process
condition (Putun et al., 2002). As usual, the pyrolysis processes under development are
based on two different concepts: slow pyrolysis and fast or flash pyrolysis. These differ
from each other in terms of chemistry, overall yields and quality of products.
2.6 Pyrolysis Process Types
2.6.1 Slow Pyrolysis
Slow pyrolysis has been applied for thousands of years and has been mainly used
for the production of charcoal. In slow pyrolysis, biomass typically was heated to 500 ºC.
The vapor residence time varies from 5 to 30 minute (Mohan et al., 2006).
Putun et al. (2001) had conducted fixed bed pyrolysis of Euphorbia rigida,
sunflower presses bagasse and hazelnut shell, at different temperatures and heating rate of 7
K/min. Product yield was found to increase in all the three cases when the pyrolysis
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temperature was increased from 673 to 973 K. Their findings are as shown in Table 2.1 for
increasing of N2 flow rate.
Table 2.1: Percent yields of products (approx.) from various biomasses at different
temperatures (Putun et al., 2001).
Euohorbia rigida673773973
Sunflower673773973
Hazelnut shell673773973
442821
Product Yield (%)Char Oil Water
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17
36
243226
3644
21
352726
4741
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Temp. (K)
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121212
13
38
2023
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Slow pyrolysis of cottonseed cake at heating rates of 7 ºC/min in a tubular reactor
was reported by Ozbay et al. (2001). Pyrolysis works were conducted in two reactors,
Heinz retort and a well-swept tubular reactor. From results shown in Table 2.2, it was seen
that with the increase in the temperature the oil yield increased up to 600 ºC but decreased
at around 750 ºC. Char yield showed continuous decrease. Oil yield was maximum at N2
flow rate of 100 cm3/min.